EP3792576A1 - Wärmeübertragungsvorrichtung mit einer fluidleitung - Google Patents

Wärmeübertragungsvorrichtung mit einer fluidleitung Download PDF

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Publication number
EP3792576A1
EP3792576A1 EP20206065.3A EP20206065A EP3792576A1 EP 3792576 A1 EP3792576 A1 EP 3792576A1 EP 20206065 A EP20206065 A EP 20206065A EP 3792576 A1 EP3792576 A1 EP 3792576A1
Authority
EP
European Patent Office
Prior art keywords
fluid conduit
thermal transfer
channels
transfer device
longitudinally
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP20206065.3A
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English (en)
French (fr)
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EP3792576B1 (de
Inventor
Henri Klaba
Ali Chehade
Hadrien Bauduin
Angelos Lyris
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OVH SAS
Original Assignee
OVH SAS
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Publication date
Application filed by OVH SAS filed Critical OVH SAS
Priority to DK20206065.3T priority Critical patent/DK3792576T3/da
Priority to EP20206065.3A priority patent/EP3792576B1/de
Priority to PL20206065.3T priority patent/PL3792576T3/pl
Publication of EP3792576A1 publication Critical patent/EP3792576A1/de
Application granted granted Critical
Publication of EP3792576B1 publication Critical patent/EP3792576B1/de
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Anticipated expiration legal-status Critical

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/03—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
    • F28D1/0308—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other
    • F28D1/035—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other with U-flow or serpentine-flow inside the conduits
    • G—PHYSICS
    • G06—COMPUTING; CALCULATING OR COUNTING
    • G06F—ELECTRIC DIGITAL DATA PROCESSING
    • G06F1/00—Details not covered by groups G06F3/00 - G06F13/00 and G06F21/00
    • G06F1/16—Constructional details or arrangements
    • G06F1/20—Cooling means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/08—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by varying the cross-section of the flow channels
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/12—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/12—Elements constructed in the shape of a hollow panel, e.g. with channels
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L23/00—Details of semiconductor or other solid state devices
    • H01L23/34—Arrangements for cooling, heating, ventilating or temperature compensation ; Temperature sensing arrangements
    • H01L23/46—Arrangements for cooling, heating, ventilating or temperature compensation ; Temperature sensing arrangements involving the transfer of heat by flowing fluids
    • H01L23/473—Arrangements for cooling, heating, ventilating or temperature compensation ; Temperature sensing arrangements involving the transfer of heat by flowing fluids by flowing liquids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0028—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for cooling heat generating elements, e.g. for cooling electronic components or electric devices
    • F28D2021/0029—Heat sinks
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2210/00—Heat exchange conduits
    • F28F2210/02—Heat exchange conduits with particular branching, e.g. fractal conduit arrangements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2210/00—Heat exchange conduits
    • F28F2210/10—Particular layout, e.g. for uniform temperature distribution
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2250/00—Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
    • F28F2250/10—Particular pattern of flow of the heat exchange media
    • F28F2250/102—Particular pattern of flow of the heat exchange media with change of flow direction
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2250/00—Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
    • F28F2250/10—Particular pattern of flow of the heat exchange media
    • F28F2250/108—Particular pattern of flow of the heat exchange media with combined cross flow and parallel flow
    • G—PHYSICS
    • G06—COMPUTING; CALCULATING OR COUNTING
    • G06F—ELECTRIC DIGITAL DATA PROCESSING
    • G06F2200/00—Indexing scheme relating to G06F1/04 - G06F1/32
    • G06F2200/20—Indexing scheme relating to G06F1/20
    • G06F2200/201—Cooling arrangements using cooling fluid
    • H—ELECTRICITY
    • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K7/00—Constructional details common to different types of electric apparatus
    • H05K7/20—Modifications to facilitate cooling, ventilating, or heating
    • H05K7/20218—Modifications to facilitate cooling, ventilating, or heating using a liquid coolant without phase change in electronic enclosures
    • H05K7/20254—Cold plates transferring heat from heat source to coolant

Definitions

  • the present technology relates to thermal transfer devices having a fluid conduit.
  • Heat dissipation is an important consideration for computer systems. Notably, many components of a computer system, such as a processor (also referred to as central processing unit (CPU)), generate heat and thus require cooling to avoid performance degradation and, in some cases, failure. Moreover, with advancing technological progress, processors are not only becoming more performant but also have a greater associated thermal design power (TDP) (i.e., a maximum amount of heat generated thereby which a cooling system should dissipate).
  • TDP thermal design power
  • heat sinks which rely on a heat transfer medium (e.g., a gas or liquid) to carry away the heat generated by a particular component of the computer system.
  • a heat transfer medium e.g., a gas or liquid
  • a water block which is a watercooling heat sink, is thermally coupled to the component to be cooled (e.g., the processor) and water is circulated through a conduit in the water block to absorb the heat from the component. As water flows out of the water block, so does the heat absorbed thereby.
  • water blocks are susceptible to clogging and, in some cases, can be expensive to produce as manufacturing thereof can be time-consuming.
  • the increasing cooling requirements of processors and other such components pose a challenge to water blocks.
  • conventional water blocks are typically efficient only when operating with a relatively high water flow rate and at high pressure and thus require a pump system (for feeding water to the water block) with an accordingly high static head.
  • a thermal transfer device for a heat-generating electronic component.
  • the thermal transfer device includes a body having a thermal transfer surface configured to be placed in contact with the heat-generating electronic component.
  • the thermal transfer device also includes a fluid conduit defined in the body and configured for conveying fluid through the body.
  • the fluid conduit is thermally coupled to the thermal transfer surface.
  • the fluid conduit has an inlet and an outlet.
  • the fluid conduit forms a serpentine path.
  • the fluid conduit branches into at least two channels extending generally parallel to one another along the serpentine path formed by the fluid conduit.
  • Each of the at least two channels defines a sinusoidal pattern along at least a majority of a span thereof.
  • the at least two channels merge at a second junction.
  • the first junction is the inlet of the fluid conduit.
  • the second junction is the outlet of the fluid conduit.
  • the serpentine path formed by the fluid conduit defines a plurality of longitudinally-extending sections that are parallel to one another and laterally spaced from one another.
  • the plurality of longitudinally-extending sections includes a first longitudinally-extending section and a second longitudinally-extending section that are laterally furthest-most of the longitudinally-extending sections.
  • the first junction is located at the first longitudinally-extending section and the second junction is located at the second longitudinally-extending section.
  • a width of each of the at least two channels is constant.
  • the width of each of the at least two channels is between 1 mm and 4 mm inclusively.
  • the second junction is a first intermediate junction downstream from the first junction; the fluid conduit branches into an other at least two channels at a second intermediate junction between the first intermediate junction and the outlet; between the first and second intermediate junctions, the fluid conduit defines a plurality of longitudinally-extending sections that are parallel to one another and laterally spaced from one another, the fluid conduit having a single channel extending along the longitudinally-extending sections; the longitudinally-extending sections are substantially laterally centered between lateral ends of the body; and the other at least two channels merge at a fourth junction.
  • each of the other at least two channels defines a sinusoidal pattern along at least a majority of a span thereof.
  • the serpentine path of the fluid conduit extends from the inlet to the outlet.
  • the body comprises a first body portion and a second body portion affixed to the first body portion; the fluid conduit is defined by the first and second body portions; and a path of each of the at least two channels is defined by the first body portion.
  • the inlet and the outlet are defined in the second body portion.
  • the first and second body portions are welded to one another.
  • the thermal transfer device is a water block.
  • the water block is generally rectangular.
  • the inlet and the outlet are generally located at diagonally opposite corners of the rectangular water block.
  • Embodiments of the present technology each have at least one of the above-mentioned objects and/or aspects, but do not necessarily have all of them. It should be understood that some aspects of the present technology that have resulted from attempting to attain the above-mentioned object may not satisfy this object and/or may satisfy other objects not specifically recited herein.
  • Figure 1 illustrates a thermal transfer device 10 for cooling a target component 105.
  • the target component 105 is a central processing unit (CPU) of a computer system 100 and is mounted to a motherboard 102 thereof.
  • the CPU 105 generates a significant amount of heat and, as is known, can benefit from cooling.
  • the target component 105 could be any other suitable heat-generating component (e.g., a graphics processing unit (GPU)) or an intermediary component disposed between the thermal transfer device 10 and a heat-generating component.
  • a graphics processing unit GPU
  • the thermal transfer device 10 is a water block (i.e., a heat sink that uses water as a fluid medium for transferring heat) and will be referred to as such herein. It is nevertheless contemplated that a fluid other than water could be used in other embodiments.
  • the water block 10 has a body 12 including two body portions 13, 14 that are affixed to one another.
  • the body portions 13, 14 may be thought of as a cover 13 and a base 14 respectively.
  • the body 12 (as well as each of the cover 13 and the base 14 thereof) is rectangular, with the cover 13 and the base 14 having identical lengths and widths such that, when the cover 13 is secured to the base 14, as shown in Figure 1 , the ends of the cover 13 and the base 14 are substantially flush with one another.
  • the cover 13 and the base 14 are made of copper and are welded to one another. More specifically, the cover 13 is soldered onto the base 14. In other embodiments, the cover 13 and the base 14 could be cold-welded or laser-welded together.
  • the welding of the cover 13 and the base 14 prevents fluid leaks from the water block 10 without using any sealing members (e.g., a packing). Moreover, welding of the cover 13 and the base 14 allows using fewer elements such as screws or other fasteners for holding the cover 13 and the base 14 together.
  • the water block 10 is thermally coupled to the CPU 105 for cooling thereof. More specifically, the body 12 has an external thermal transfer surface 20 (which is a lower surface of the base 14) that is placed in contact with the CPU 105. As shown in Figure 2 , the thermal transfer surface 20 is placed in contact with an upper surface of the CPU 105 to absorb heat therefrom.
  • a thermal paste may be disposed between the thermal transfer surface 20 and the CPU 105, applied to the thermal transfer surface 20 or the upper surface of the CPU 105, to improve heat transfer therebetween by ensuring continuity of contact between the thermal transfer surface 20 and the upper surface of the CPU 105. Any other medium with adequate thermal conductivity for ensuring continuity of contact between the thermal transfer surface 20 and the upper surface of the CPU 105 may be used instead of the thermal paste in other cases.
  • the water block 10 has a fluid conduit 30 defined in the body 12 for conveying water therethrough. More specifically, the fluid conduit 30 is defined by surfaces of both the cover 13 and the base 14. Notably, a continuous recess 15 formed in the upper surface 24 of the base 14 defines a path describes by the fluid conduit 30.
  • the fluid conduit 30 is thermally coupled to the thermal transfer surface 20 such that, when water flows in the fluid conduit 30, heat absorbed by the thermal transfer surface 20 is subsequently absorbed by water flowing in the fluid conduit 30.
  • Water is received into the fluid conduit 30 via an inlet 32 and expelled therefrom via an outlet 34.
  • Both the inlet 32 and the outlet 34 are defined in the cover 13 (i.e., water enters and exits the body 12 via the cover 13).
  • the inlet 32 is fluidly connected to a tube 16 through which water is fed into the fluid conduit 30.
  • a tube 18 is fluidly connected to the outlet 34 to discharge water from the fluid conduit 30.
  • the tubes 16, 18 are copper tubes and are welded to the outer surface 22 of the body 12 (i.e., an outer surface of the cover 13).
  • the fluid conduit 30 describes a path from the inlet 32 to the outlet 34 such as to guide the flow of water along the path. As will be described in greater detail below, the particular path described by the fluid conduit 30 may provide more efficient cooling of the CPU 105.
  • the path described by the fluid conduit 30 begins at the inlet 32 thereof which is laterally centered on the water block 10. That is, as best seen in Figure 3 , the inlet 32 is located centrally between the lateral ends of the water block 10 (and thus the lateral ends 29, 31 of the base 14).
  • the fluid conduit 30 branches into two channels 36 1 , 36 2 at the inlet 32 such that the flow of fluid within the fluid conduit 30 is split between both channels 36 1 , 36 2 . This may promote laminar flow of fluid within the fluid conduit 30 which reduces pressure drop of the fluid as it flows through the fluid conduit 30.
  • the channels 36 1 , 36 2 merge together again at the outlet 34. However, in the span of the fluid conduit 30 between the inlet 32 and the outlet 34, the channels 36 1 , 36 2 are fluidly separate from one another such that water flow from both channels 36 1 , 36 2 does not mix until reaching the outlet 34.
  • the junction at which the fluid conduit 30 branches into the two channels 36 1 , 36 2 could be at a location other than the inlet 32.
  • the fluid conduit 30 could branch into the two channels 36 1 , 36 2 at a junction downstream from the inlet 32 (i.e., a location, along the path of the fluid conduit 30, further from the inlet 32).
  • the junction at which the two channels 36 1 , 36 2 merge together could be upstream from the outlet 34.
  • the path of the fluid conduit 30 (including the path of each of the channels 36 1 , 36 2 ) is defined by the base 14 independently of the cover 13.
  • the cover 13 defines part of the fluid conduit 30 (covering an open top thereof)
  • the direction of the water flow within the fluid conduit 30 is defined by the recess 15 machined into the upper surface 24 of the base 14.
  • the cover 13 has a lower flat surface that closes the open top of the recess 15 (except at the inlet 32 and the outlet 34).
  • the channels 36 1 , 36 2 extend adjacent and parallel to one another along an initial portion 38 of the fluid conduit 30 beginning at the junction at which the channels 36 1 , 36 2 begin (i.e., at the inlet 32 in this embodiment).
  • the initial portion 38 is the portion of the fluid conduit 30 along which the channels 36 1 , 36 2 are closest to one another aside from when the channels 36 1 , 36 2 merge again at the outlet 34.
  • the channels 36 1 , 36 2 diverge from one another such that each of the channels 36 1 , 36 2 forms a "serpentine" path.
  • serpentine paths of the channels 36 1 , 36 2 extend toward generally opposite lateral directions (i.e., one extends toward the lateral end 29 while the other extends toward the opposite lateral end 31).
  • a serpentine path is herein defined as being a path that describes at least one S-shaped curve.
  • the serpentine path formed by each of the channels 36 1 , 36 2 includes a plurality of longitudinally-extending sections that extend generally longitudinally and which are connected by looping sections.
  • the channel 36 1 has a plurality of longitudinally-extending sections 40 1 -40 7 that are parallel to one another and are laterally spaced from one another, with adjacent ones of the longitudinally-extending sections 40 1 -40 7 being connected by looping sections 44 1 -44 6 .
  • the longitudinally-extending section 40 1 is an innermost one of the longitudinally-extending sections 40 1 -40 7 (i.e., furthest away from the lateral end 31) and is part of the initial portion 38.
  • the longitudinally-extending section 40 7 is an outermost one of the longitudinally-extending sections 40 1 -40 7 (i.e., closest to the lateral end 31).
  • the channel 36 2 has a plurality of longitudinally-extending sections 42 1 -42 7 that are parallel to one another, with adjacent ones of the longitudinally-extending sections 42i-42 7 being connected by looping sections 46 1 -46 6 .
  • the longitudinally-extending section 42 1 is an innermost one of the longitudinally-extending sections 42 1 -42 7 (i.e., furthest away from the lateral end 29) and part of the initial portion 38.
  • the longitudinally-extending section 42 7 is an outermost one of the longitudinally-extending sections 42 1 -42 7 (i.e., closest to the lateral end 29).
  • the longitudinally-extending sections 40 1 -40 7 , 42 1 -42 7 of the channels 36 1 , 36 2 have approximately the same length. This spreads the heat transfer capability more evenly throughout the thermal transfer surface 20 of the water block 10.
  • the innermost longitudinally-extending sections 40 1 , 42 1 of the channels 36 1 , 36 2 extend adjacent and parallel to one another along the initial portion 38 of the fluid conduit 30. As such, the innermost longitudinally-extending sections 40 1 , 42 1 are laterally aligned with the inlet 32 which, as mentioned above, is laterally centered between the lateral ends 29, 31 of the base 14 (and thus the lateral ends of the water block 10).
  • the inlet 32 is also located centrally between the outermost longitudinally-extending section 40 7 of the channel 36 1 and the outermost longitudinally-extending section 42 7 of the channel 36 2 .
  • each of the channels 36 1 , 36 2 defines a sinusoidal pattern along a majority of a span thereof. That is, each one of the channels 36 1 , 36 2 has a repetitive pattern approximating that of a sinusoidal function along at least half of the span of that channel 36 1 , 36 2 .
  • the sinusoidal pattern is defined along the longitudinally-extending portions 40 1 -40 7 , 42 1 -42 7 of the serpentine paths formed by the channels 36 1 , 36 2 .
  • the sinusoidal pattern defined by the channels 36 1 , 36 2 changes a direction of the flow of water within the channels 36 1 , 36 2 as the flow of water engages the curves defined by the sinusoidal pattern.
  • the channels 36 1 , 36 2 have a constant width (i.e., a distance between the opposite walls of each of the channels 36 1 , 36 2 is uniform along a span thereof) as the width is unaffected by the curves defined by the sinusoidal pattern.
  • the width of each of the channels 36 1 , 36 2 is approximately 2 mm. In other embodiments, the width of each of the channels 36 1 , 36 2 may be between 1 mm and 4 mm inclusively.
  • This relatively large width of the channels 36 1 , 36 2 allows using simple and fast manufacturing methods to produce the water block 10 in contrast with some conventional water blocks having "micro" channels made via electrical discharge machining.
  • the channels 36 1 , 36 2 of the water block 10 can be machined (e.g., via a mill) with a tool having an adequate diameter. Therefore, this results in a more economic manufacturing process for producing the water block 10.
  • the relatively large width of the channels 36 1 , 36 2 may be helpful to restrict pressure drop of the water flow within the channels 36 1 , 36 2 , as well as to limit fouling of the channels 36 1 , 36 2 .
  • the channels 36 1 , 36 2 may have any other suitable dimensions in other embodiments, so long as it is convenient for the flow regime within the channels 36 1 , 36 2 and easily machinable such as with a machine tool having a rotary cutter (e.g., a mill or a router).
  • a rotary cutter e.g., a mill or a router
  • the sinusoidal pattern defined by the channels 36 1 , 36 2 advantageously increases the contact area of the walls thereof compared to if the channels 36 1 , 36 2 were linear (i.e., straight). This increased contact area results in improved heat transfer.
  • the sinusoidal pattern also creates flow disturbances leading to greater friction between the water and the walls of the channels 36 1 , 36 2 which also improves heat transfer therebetween and, moreover, limits the fouling rate and clogging within the channels 36 1 , 36 2 , while generating a limited increase of pressure drop compared to if the channels 36 1 , 36 2 were linear.
  • the channels 36 1 , 36 2 diverge to extend generally laterally (i.e., perpendicular to the outermost longitudinally-extending sections 40 7 , 42 7 ) toward one another and then merge at the outlet 34.
  • the channels 36 1 , 36 2 extend in opposite directions from the outlet 34. It is noted that the outlet 34 is laterally aligned with the inlet 32 such that the outlet 34 is laterally centered between the ends 29, 31 of the base 14.
  • the junction at which the two channels 36 1 , 36 2 merge could be at a location other than the outlet 34.
  • the two channels 36 1 , 36 2 could merge at a junction upstream from the outlet 34 (i.e., a location, along the path of the fluid conduit 30, further from the outlet 34).
  • the above-described configuration of the fluid conduit 30 allows routing relatively cool water to a target area 106, as shown in Figure 3 .
  • the target area 106 corresponds to a hottest zone of the CPU 105. That is, the target area 106 is an area of the water block 10 which, when the water block 10 is installed on the CPU 105, overlies a point of the CPU 105 that exhibits a highest temperature during operation. As such, the target area 106 can benefit from being exposed to water that is as cool as possible.
  • a distance along the fluid conduit 30 between the inlet 32 and the target area 106 is made relatively small since the inlet 32 is where water flowing within the fluid conduit 30 is coldest because heat has not yet substantially been transferred to the water.
  • the inlet 32 is located centrally between the lateral ends 29, 31 such as to be laterally aligned with the target area 106 and thus be relatively close thereto while at the same time allowing the fluid conduit 30 to overlap a majority of the area of the thermal transfer surface 20.
  • the initial portion 38 which is the portion of the fluid conduit 30 along which water flowing in the fluid conduit 30 is coldest due to its proximity to the inlet 32, overlaps the target area 106 such as to bring the cool water from the inlet 32 to the target area 106 relatively quickly before the water absorbs a substantial amount of heat.
  • the inlet and the outlet of the fluid conduit are located at opposite corners of the water block and thus the water travels a substantial distance (e.g., in a serpentine path) before it gets to the area corresponding to the hottest zone of the CPU or other component to be cooled.
  • a substantial amount of heat has already been transferred to the water thus making it less efficient at absorbing heat from the hottest zone of the CPU.
  • This configuration of the fluid conduit 30, and those described below with respect to other embodiments thereof, allows the water block 10 to operate efficiently at a relatively low flow rate and low pressure, with limited pressure drop in the water flow. Moreover, due the lower flow rate and pressure operating parameters of the water block 10, a pump needed for feeding the water block 10 can have a lower static head than if it were used for feeding a conventional water block that operates efficiently only at high flow rate and high pressure. Alternatively or additionally, the lower flow rate and pressure operating parameters of the water block 10 can allow a single pump to simultaneously feed multiple water blocks such as the water block 10. This is particularly useful in cases where multiple components have to be cooled such as, for example, in a data center storing multiple servers that require cooling.
  • the lower flow rate and pressure needed for efficient operation of the water block 10 can also carry over to the water circulation system to which the water block 10 is coupled.
  • the water flow in the water circulation system is also subject to reduced pressure drop.
  • the diameter of the tubing within which the water circulates in the water circulation system of the data center can also be reduced which, while causing an increase in the pressure drop in the water flow, results in a more compact water circulation system that is less costly and easier to install.
  • a risk of leaks in the water circulation system is also reduced since the water circulation system is less pressurized.
  • heat collected by the water blocks 10 leads to a temperature increase in the water circulation system which may be more convenient to design and operate the heat exchangers (e.g., chillers, dry coolers, plate heat exchangers) that are coupled to the water circulation system for releasing the heat collected by the water blocks 10.
  • this temperature increase in the water circulation system may lead to high outlet temperature, which may ease heat valorization (e.g. heating buildings in the winter).
  • the water block 10 could operate at high inlet temperatures of up to 50°C, whereby water chillers for the water circulation system of the data center can be replaced by more preferable direct cooling solutions (e.g., dry coolers), which reduces costs and energy consumption associated with the implementation of water chillers.
  • direct cooling solutions e.g., dry coolers
  • the fluid conduit 30 of the above-described embodiment is replaced with a fluid conduit 130.
  • the path described by the fluid conduit 130 as defined by the base 14 is different from the fluid conduit 30 described above.
  • the fluid conduit 130 is thermally coupled to the thermal transfer surface 20 such that, when water flows in the fluid conduit 130, heat absorbed by the thermal transfer surface 20 is subsequently absorbed by water flowing in the fluid conduit 130.
  • Water is received into the fluid conduit 130 via an inlet 132 and expelled therefrom via an outlet 134. Both the inlet 132 and the outlet 134 are defined in the cover 13 (i.e., water enters and exits the body 12 via the cover 13).
  • the path described by the fluid conduit 130 begins at the inlet 132 thereof which is located generally at a corner of the rectangular water block 10. That is, the inlet 132 is located adjacent an intersection of the longitudinal end 25 and the lateral end 31 of the base 14.
  • the fluid conduit 130 branches into two channels 136 1 , 136 2 at the inlet 32 such that the flow of fluid within the fluid conduit 130 is split between both channels 136 1 , 136 2 . As discussed above, this may promote laminar flow of fluid within the fluid conduit 130 which reduces pressure drop of the fluid as it flows through the fluid conduit 130.
  • the channels 136 1 , 136 2 extend parallel to one another along at least a majority of a span of the fluid conduit 130.
  • the channels 136 1 , 136 2 extend parallel and adjacent to one another from the inlet 132 to the outlet 134. As will be described further below, the channels 136 1 , 136 2 merge together again at the outlet 134. However, in the span of the fluid conduit 130 between the inlet 132 and the outlet 134, the channels 136 1 , 136 2 are fluidly separate from one another such that water flow from both channels 136 1 , 136 2 does not mix until reaching the outlet 134.
  • the fluid conduit 130 could branch into more than two channels.
  • the fluid conduit could branch into three channels or four channels.
  • the junction at which the fluid conduit 130 branches into the two channels 136 1 , 136 2 could be at a location other than the inlet 132.
  • the fluid conduit 130 could branch into the two channels 136 1 , 136 2 at a junction downstream from the inlet 132 (i.e., a location, along the path of the fluid conduit 130, further from the inlet 132).
  • the junction at which the two channels 136 1 , 136 2 merge together could be upstream from the outlet 134.
  • the fluid conduit 130 forms a "serpentine" path.
  • a serpentine path is herein defined as being a path that describes at least one S-shaped curve.
  • the fluid conduit 130 defines a plurality of longitudinally-extending sections 140 1 -140 7 that are parallel to one another and are laterally spaced from one another, with adjacent ones of the longitudinally-extending sections 140 1 -140 7 being connected by looping sections 144 1 -144 6 .
  • the channels 136 1 , 136 2 of the fluid conduit 130 extend generally parallel to one another along the serpentine path (i.e., along the longitudinally-extending sections 140 1 -140 7 and the looping sections 144 1 -144 6 ).
  • the inlet 132 is located at the longitudinally-extending section 140 1 and the outlet 134 is located at the longitudinally-extending section 140 7 such that the inlet 132 and the outlet 134 are located at the laterally furthest-most of the longitudinally-extending sections 140 1 -140 7 respectively (i.e., the longitudinally-extending sections 140 1 -140 7 which are most laterally spaced from one another).
  • the inlet 132 and the outlet 134 are generally located at diagonally opposite corners of the rectangular water block 10 (like illustrated in Figure 4 , with an even number of looping sections 144 1 -144 6 ).
  • the tubes 16, 18 will be connected to the cover 13 at the corresponding diagonally opposite corners (unlike what is illustrated in Figure 1 ) to be connected to the inlet 132 and the outlet 134.
  • the inlet 132 and the outlet 134 may be located at laterally opposite corners adjacent the same longitudinal end 25. In such embodiments, the number of looping sections 144 x would be uneven (see looping sections 144 1 -144 5 in Figure 7 ).
  • the two channels 136 1 , 136 2 could merge together at an intermediate junction between the inlet 132 and the outlet 134, such that the fluid conduit 130 defines a single channel downstream of the intermediate junction before the fluid conduit 130 splits again into two channels 146 1 , 146 2 .
  • the longitudinally-extending sections 140 1 -140 3 are positioned, laterally, between the inlet 132 and an intermediate junction JCT 1 .
  • the two channels 136 1 , 136 2 extend along each of the longitudinally-extending sections 140 1 -140 3 and looping sections 144 1 , 144 2 interconnecting the longitudinally-extending sections 140 1 -140 3 .
  • the two channels 136 1 , 136 2 merge into a single channel 155 which, alone, defines the path of the fluid conduit 130 from the intermediate junction JCT 1 to another intermediate junction JCT 2 downstream from the intermediate junction JCT 1 .
  • the fluid conduit 130 defines a plurality of longitudinally-extending sections 145 1 -145 3 that are parallel to one another and laterally spaced from one another, and extending between the intermediate junctions JCT 1 , JCT 2 .
  • the single channel 155 extends along the longitudinally-extending sections 145 1 -145 3 and the looping sections interconnecting the longitudinally-extending sections 145 1 -145 3 .
  • the longitudinally-extending sections 145 1 -145 3 are substantially laterally centered between the lateral ends 29, 31 and define a limited region of the fluid conduit 130 where heat transfer is prioritized over pressure drop. This may be beneficial for example in cases where heat generation of the CPU 105 is greatest at its center.
  • the fluid conduit 130 again branches into two channels 146 1 , 146 2 at the intermediate junction JCT 2 downstream from the intermediate junction JCT 1 . Between the intermediate junction JCT 2 and the outlet 134, the fluid conduit 130 defines longitudinally-extending sections 140 4 -140 6 positioned parallel to one another and laterally spaced from one another, similarly to the previous longitudinally-extending sections 140 1 -140 3 .
  • the two channels 146 1 , 146 2 extend along each of the longitudinally-extending sections 140 4 -140 6 and looping sections 144 3 , 144 4 interconnecting the longitudinally-extending sections 140 4 -140 6 .
  • the two channels 146 1 , 146 2 are configured similarly to the channels 136 1 , 136 2 - notably, the two channels 146 1 , 146 2 extend parallel to one another along at least a majority (i.e., a majority or an entirety) of a span thereof and each of the channels 146 1 , 146 2 also defines a sinusoidal pattern along at least a majority of a span thereof.
  • the channels 146 1 , 146 2 merge at the outlet 134 downstream from the intermediate junction JCT 2 .
  • the outlet 134 is located at a diagonally opposite corner from the inlet 132.
  • the inlet 132 and the outlet 134 may be located at laterally opposite corners adjacent the same longitudinal end 25, as discussed above with regard to Figure 7 .
  • Each of the channels 136 1 , 136 2 defines a sinusoidal pattern along a majority of a span thereof. That is, each one of the channels 136 1 , 136 2 has a repetitive pattern approximating that of a sinusoidal function along at least half of the span of that channel 136 1 , 136 2 .
  • the sinusoidal pattern is defined along the longitudinally-extending portions 140 1 -140 7 of the serpentine path of the fluid conduit 130.
  • the sinusoidal pattern defined by the channels 136 1 , 136 2 changes a direction of the flow of water within the channels 136 1 , 136 2 as the flow of water engages the curves defined by the sinusoidal pattern.
  • the channels 136 1 , 136 2 have a constant width (i.e., a distance between the opposite walls of each of the channels 136 1 , 136 2 is uniform along a span thereof) as the width is unaffected by the curves defined by the sinusoidal pattern.
  • the width of each of the channels 136 1 , 136 2 is 2 mm.
  • the width of the channels of each of the channels 136 1 , 136 2 may be between 1 mm and 4 mm.
  • the channels 136 1 , 136 2 may have any other suitable dimensions in other embodiments so long as it is convenient for the flow regime within the channels 136 1 , 136 2 and easily machinable such as with a machine tool having a rotary cutter (e.g., a mill or a router).
  • a rotary cutter e.g., a mill or a router
  • the fluid conduit 130 is defined by the cover 13 and the base 14 when the cover 13 and the base 14 are affixed to one another.
  • the path of the fluid conduit 130 (including the path of each of the channels 136 1 , 136 2 ) is defined by the base 14 independently of the cover 13.
  • the cover 13 defines part of the fluid conduit 130 (covering an open top thereof)
  • the direction of the water flow within the fluid conduit 30 is defined by the recess 115 machined into the upper surface 24 of the base 14.
  • the cover 13 has a lower flat surface that closes the open top of the recess 115 (except at the inlet 132 and the outlet 134).
  • the fluid conduit 30 is replaced with a fluid conduit 230.
  • the path described by the fluid conduit 230 as defined by the base 14 is different from the fluid conduits 30, 130 described above.
  • the fluid conduit 230 is thermally coupled to the thermal transfer surface 20 such that, when water flows in the fluid conduit 230, heat absorbed by the thermal transfer surface 20 is subsequently absorbed by water flowing in the fluid conduit 230.
  • Water is received into the fluid conduit 230 via an inlet 232 and expelled therefrom via an outlet 234. Both the inlet 232 and the outlet 234 are defined in the cover 13 (i.e., water enters and exits the body 12 via the cover 13).
  • the path described by the fluid conduit 230 begins at the inlet 232 thereof which is located generally centrally of the rectangular water block 10 (i.e., laterally and longitudinally centered between the lateral and longitudinal ends thereof).
  • the central position of the inlet 232 allows routing cool water to the center of the water block 10, which may be beneficial if the location of the CPU 105 that is most desired to be cooled is centrally located.
  • water will be coolest along the fluid conduit 230 at the central inlet 232 (since the water has not yet absorbed heat from circulating through an appreciable span of the fluid conduit 230) and therefore heat transfer at the center of the CPU 105 (i.e., a position aligned with the inlet 232) will be significant.
  • the fluid conduit 230 branches into two channels 236 1 , 236 2 at the inlet 232 such that the flow of fluid within the fluid conduit 230 is split between both channels 236 1 , 236 2 . As discussed above, this may promote laminar flow of fluid within the fluid conduit 230 which reduces pressure drop of the fluid as it flows therethrough.
  • the channels 236 1 , 236 2 extend parallel to one another along at least a majority of a span of the fluid conduit 230. More specifically, in this embodiment, the channels 236i, 236 2 extend parallel from the inlet 232 to the outlet 234. As will be described further below, the channels 236 1 , 236 2 merge together again at the outlet 234. However, in the span of the fluid conduit 230 between the inlet 232 and the outlet 234, the channels 236 1 , 236 2 are fluidly separate from one another such that water flow from both channels 236i, 236 2 does not mix until reaching the outlet 234.
  • the fluid conduit 230 could branch into more than two channels.
  • the fluid conduit could branch into three channels or four channels.
  • the junction at which the fluid conduit 230 branches into the two channels 236 1 , 236 2 could be at a location other than the inlet 232.
  • the fluid conduit 230 could branch into the two channels 236 1 , 236 2 at a junction JCT downstream from the inlet 232 (i.e., a location, along the path of the fluid conduit 230, further from the inlet 232). This configuration may be advantageous to prioritize heat transfer at a given region of the fluid conduit 230.
  • heat transfer in the region from the inlet 232 to the junction JCT may be greater than in the remainder of the fluid conduit 230 while incurring some pressure drop in the water in this limited region of the fluid conduit 230 (since the water flow is not split into the two channels 236 1 , 236 2 in this region).
  • the junction at which the two channels 236 1 , 236 2 merge together could be upstream from the outlet 234.
  • Each of the channels 236 1 , 236 2 has a constant width (i.e., a distance between the opposite walls of each of the channels 236 1 , 236 2 is uniform along a span thereof).
  • the width of each of the channels 236i, 236 2 is 2 mm.
  • the width of the channels of each of the channels 236 1 , 236 2 may be between 1 mm and 4 mm.
  • the channels 236 1 , 236 2 may have any other suitable dimensions in other embodiments, so long as it is convenient for the flow regime within the channels 236 1 , 236 2 and easily machinable such as with a machine tool having a rotary cutter (e.g., a mill or a router).
  • the fluid conduit 230 forms a generally rectangular spiral path centered about the inlet 232. More specifically, the path of the fluid conduit 230 begins at the inlet 232 and extends further away from the inlet 232 as it revolves around the inlet 232. The spiral path of the fluid conduit 230 ends at the outlet 234 which is positioned at an outer periphery of the spiral path formed by the fluid conduit 230. In particular, the spiral path of the fluid conduit 230 is formed by ring sections 250 1 -250 5 of the fluid conduit 230. The ring sections 250 1 -250 5 are concentric about the inlet 232. The innermost ring section 250 1 is closest to the inlet 232 and the outermost ring section 250 5 is furthest form the inlet 232.
  • the outlet 234 is located at the outermost ring section 250s. Since the outlet 234 is located generally at a corner of the rectangular water block 10, the spiral path of the fluid conduit 230 spreads across almost an entirety of the area of the water block 10 (i.e., the recess 215 in the upper surface 24 of the base 14 spans most of a length and a width of the base 14).
  • the rectangular spiral path of the fluid conduit 230 is generally square (i.e., the length and width of the fluid conduit 230 are approximately similar). However, in some cases, the length of the spiral path of the fluid conduit 230 be greater than its width. This may better accommodate the rectangular shape of the CPU 105 (or other component to be cooled).
  • the spiral path of the fluid conduit 230 does not include many tight curves (i.e., the radius of curvature of most if not all curves is relatively large) which facilitates and speeds up machining of the recess 215 in the base 14.
  • the radius of curvature of the curves of the spiral path may increase in proportion to a distance of the curve relative to the inlet 232. That is, the further from the central inlet 232 a curve of the spiral path is, the greater its radius of curvature.
  • the fluid conduit 230 is defined by the cover 13 and the base 14 when the cover 13 and the base 14 are affixed to one another.
  • the path of the fluid conduit 230 (including the path of each of the channels 236 1 , 236 2 ) is defined by the base 14 independently of the cover 13.
  • the cover 13 defines part of the fluid conduit 230 (covering an open top thereof)
  • the direction of the water flow within the fluid conduit 230 is defined by the recess 215 machined into the upper surface 24 of the base 14.
  • the cover 13 has a lower flat surface that closes the open top of the recess 215 (except at the inlet 132 and the outlet 134).
  • the cover and base may be affixed to one another differently.
  • a cover 13' and a base 14' are affixed to one another by fasteners 19 (e.g., screws).
  • the cover 13' has holes extending therethrough for receiving the fasteners 19, and the base 14' has corresponding receiving openings (not shown) that are threaded to receive the fasteners 19.
  • a sealing member e.g., a gasket
  • the cover 13' is made of a polymeric material (the base 14' is still made of copper).
  • the cover 13' may be an injection molded component.
  • the tubes 16, 18 are also made of polymeric material. A resin may seal the interface between the tubes 16, 18 and the cover 13'.
  • thermal transfer device 10 has been described above as being configured for absorbing heat from the target component 105, it is contemplated that, in alternative embodiments, the thermal transfer device 10 could be used for transferring heat to the target component 105 (in such a case, the target component is not a CPU).
  • thermal transfer device 10 implemented in accordance with some non-limiting embodiments of the present technology can be represented as presented in the following numbered clauses.
EP20206065.3A 2018-09-04 2018-09-04 Wasserkühlerblock mit einer fluidleitung Active EP3792576B1 (de)

Priority Applications (3)

Application Number Priority Date Filing Date Title
DK20206065.3T DK3792576T3 (da) 2018-09-04 2018-09-04 Vandblok med en fluidledning
EP20206065.3A EP3792576B1 (de) 2018-09-04 2018-09-04 Wasserkühlerblock mit einer fluidleitung
PL20206065.3T PL3792576T3 (pl) 2018-09-04 2018-09-04 Blok wodny zawierający przewód płynowy

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP20206065.3A EP3792576B1 (de) 2018-09-04 2018-09-04 Wasserkühlerblock mit einer fluidleitung
EP18315027.5A EP3620741B1 (de) 2018-09-04 2018-09-04 Wärmeübertragungsvorrichtung mit einer fluidleitung

Related Parent Applications (2)

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EP18315027.5A Division EP3620741B1 (de) 2018-09-04 2018-09-04 Wärmeübertragungsvorrichtung mit einer fluidleitung
EP18315027.5A Division-Into EP3620741B1 (de) 2018-09-04 2018-09-04 Wärmeübertragungsvorrichtung mit einer fluidleitung

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EP3792576A1 true EP3792576A1 (de) 2021-03-17
EP3792576B1 EP3792576B1 (de) 2022-12-21

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EP20206065.3A Active EP3792576B1 (de) 2018-09-04 2018-09-04 Wasserkühlerblock mit einer fluidleitung

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US (2) US20200072565A1 (de)
EP (2) EP3620741B1 (de)
CN (1) CN110874127B (de)
CA (1) CA3052817A1 (de)
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Also Published As

Publication number Publication date
CN110874127A (zh) 2020-03-10
EP3792576B1 (de) 2022-12-21
CN110874127B (zh) 2022-07-12
US20210164738A1 (en) 2021-06-03
EP3620741B1 (de) 2021-01-27
EP3620741A1 (de) 2020-03-11
DK3792576T3 (da) 2023-01-09
PL3792576T3 (pl) 2023-02-20
US11644254B2 (en) 2023-05-09
DK3620741T3 (da) 2021-03-01
CA3052817A1 (en) 2020-03-04
PL3620741T3 (pl) 2021-05-31
US20200072565A1 (en) 2020-03-05

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